Note: Descriptions are shown in the official language in which they were submitted.
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FLOTATION D~tYER UNIT
Field of Invention
The present invention relates to a flotation dryer unit,
described in the introduction of the enclosed independent
claims, for drying a web, such as a coated paper web, and
to a method for feeding drying gas or air towards the web
to be dried in the flotation dryer unit.
The present invention especially relates to such flotation
dryer units in which drying air is blown onto the web from
air distribution channels, extending over the web and
combined with supply air distribution chambers arranged on
the side of the web.
Related Art
Various kinds of flotation dryers or cylinder groups,
lately also infra-dryers, are used for drying coated paper.
The various drying methods have different advantageous
features. The choice of dryer and the layout of drying may
have an effect, for example, on the quality of the coated
paper, energy costs, runnability of the paper web, layout
of the coating machine in general (web path draw, space
consumption etc.), and investment costs. At present, also
combinations of various dryer types are thus used for
achieving the optimum drying result, whereby the aim is to
-combine good properties of the various-types.
,In a flotation dryer, the evaporation of water from the web
is typically achieved by hot air blown onto the web surface
from nozzles. The specific evaporation of the flotation
dryer is then principally dependent on the te~erature and
velocity of air blown and also on the type of nozzle used.
Coaanonly used nozzle types comprise, for example, over
pressure and underpressure nozzles, and also direct
impingement and orifice nozzles.
Flotation dryers include the following good features: good
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runnability of paper; good energy economy; minimization of
thermal stress in the machine room; double-sided drying
possible; controlled drying as the impingement air
velocities for the upper and lower sides may be adjusted
separately; low risk of overdrying; and further, the
structure of the dryer is long-standing and durable.
However, the traditional flotation dryer has negative
features compared with, for example, an infra-dryer:
relatively low specific evaporation; relatively slow
warming up of the web a . g . of ter a break; poorer control
properties, i.e. poorer profiling; a lot space consuming;
and relatively high investment costs.
In the last few years, attempts have been made to increase
the evaporation efficiency of the flotation dryers in the
papermaking industry by increasing the blow velocity for
drying air from the typical velocity of 40 m/s to a
velocity of 60 m/s, even to 80 m/s. Also the drying air
temperature has been raised. However, increasing the blow
velocity and raising the temperature also increase the size
of the dryer, and thus the investment costs and space
consumption. These changes also increase the energy
consumption and they often have an impairing effect on the
controllability.
The air distribution system arranged in the so-called air
flotation dryer box of a traditionally constructed
flotation dryer is a three-stage system, comprising
superimposed air distribution channels both transverse and
parallel to the web path, and nozzle channels transverse to
the web path.
As blow velocities are increased, also the air volumes
blown and, thus, the height of the air flotation dryer box
become larger. In this case, the height of the air
flotation dryer box typically is already about 1.60 m, with
e.g. a web path width of 8.0 m and a blow air velocity of
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60 m/s, the efficient length of the flotation dryer in the
machine direction being about 2.4 m. Should one still wish
to increase the blow velocity, the height of the air
flotation dryer box would have to be increased still
considerably more in order to keep the flow rates of air in
the three-stage air distribution system within the limits
permitted by the design, which might, in many cases, cause
insurmountable difficulties.
The space consumed by the large height of the air flotation
dryer boxes makes it more difficult and, sometimes even
impossible, to fit the flotation dryer in connection with
a coating machine. Today, the space consumption is to a
very large extent also a matter of cost; the smaller the
space the dryers may be fitted into, the better.
Thus, it has been proposed, as is apparent, for example,
from the American patent publications US 3,964,656; US
4,021,931; and US 4,719,708, that various web floating
means with a two-stage air distribution system be used, in
which the air is led to nozzle channels travelling across
the web path directly from the side of the web path. Thus
the size and height of the air flotation dryer box may be
kept considerably smaller.
The problem with these arrangements provided with a two-
stage air distribution system is, however, how to
distribute the impingement air onto the web in an even and
controlled way and how to discharge return air evenly from
the web. Upon discharging from the nozzles onto the web,
drying air flowing over the web with a high velocity causes
vibrations and flutter in the web and tends to move the web
in the lateral direction. These kinds of movements
disadvantageous for the runnability are generated in the
web especially in high speed machines or when drying light
grade of papers. Also uneven discharge of air from the web
area generates unwanted air flows and pressure variations
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in the vicinity of the. web.
summary of the Inv~ntion
An object of the invention is thus to provide a flotation
dryer unit and a method for drying the web in a flotation
dryer unit, in which the aforementioned drawbacks present
in known arrangements are minimized.
An object of the present invention is thus especially to
provide a flotation dryer unit in which it is possible to
use higher drying air velocities than before for achieving
a good specific evaporation efficiency without impairing
the runnability.
In addition, it is an object of the invention to provide a
flotation dryer unit with good runnability and of a relati-
vely simple and light structure, which warms up and reacts
quickly to heat adjustment.
It is further an object of the invention to provide a
flotation dryer wait of simple structure, in which drying
air and return air travel as linearly as possible and in
which pressure losses and energy consumption are thus
minimized.
It is also an object of the invention to provide a
flotation dryer arrangeanent which consumes- hittle space and
which may easily . be j oined to a . variety of coating
machines.
For achieving the above mentioned objects, the flotation
dryer unit and method of the invention for feeding drying
air towards the web in a flotation dryer unit is .
characterized by what is disclosed in the characterizing
part of the independent claims.
A typical flotation dryer unit provided with a two-stage
air supply for drying a coated paper web connprises nozzle
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boxes arranged on one side or on both sides of the paper
web to be dried and extending across the web, from which
drying air is blown onto the web. Air is brought to the
nozzle boxes from a distribution chamber for supply air
5 which is common for the nozzle boxes and which lies on the
side of the dryer; air flows from the distribution chamber
to the nozzle boxes from their supply ends. The drying air
used, i.e. return air, flowing between the nozzle boxes
away from the web, is gathered from the entire back side
surface area of the dryer via a common suction chamber
covering the nozzle boxes into a return air chamber, to be
taken forward therefrom.
The air nozzle boxes are typically formed of longitudinal
box-type structures, extending over the web, and comprising
a bottom part parallel to the web plane, two side walls
typically perpendicular to the web plane and extending
across the web, and an inclined planar upper part. Due to
the inclined upper part, the nozzle boxes decline in a
wedgelike manner in the direction of the air flow.
The actual nozzle elements extending across the web are
integrated into the air distribution channel elements
extending principally across the web in the nozzle boxes;
the nozzle elements include at least one nozzle aperture or
slot, from which drying air is fed/blown towards the web.
Many types of nozzles may be used in the nozzle boxes,
preferably e.g. overpressure nozzles, such as Float nozzles
of the applicant. Also underpressure nozzles, direct
impingement nozzles or orifice nozzles may be used.
In an advantageous flotation dryer arrangement of the
invention, the height h of the air distribution channels
for the nozzle boxes perpendicular to the web declines from
the supply end of the nozzle channel towards its tail end
so that the nozzle boxes are wedge-shaped, i.e. their
height decreases in the flow direction. Thus, an even air
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supply is achieved in the entire area of the flotation
dryer unit.
Return air is led from the web area into a suction chamber
covering the nozzle boxes, and further into a common return
air chamber on the side of the dryer; the return air
chamber is typically arranged at least partially on top of
the supply air distribution chamber. In this case, also the
suction chamber preferably is wedge-shaped so that its
height increases in the flow direction of return air, i.e.
it declines from the first side of the web to the second
side.
Due to the wedge-shaped form of the nozzle boxes and the
suction box, the entire flotation dryer box is wedgelike.
Irrespective of this, the said two-stage dryer is
considerably lower than a conventional three-stage dryer,
in which supply air is led to the actual nozzle apertures
through channels arranged in three separate levels.
In the arrangement of the invention, the runnability of the
flotation dryer is further improved by preventing the
lateral flows of return air also, which is absorbed from
the web area to the space between the nozzle boxes, and by
equalizing the discharge of return air from the web area.
Return air is gathered evenly in directions both transverse
and parallel to the travelling direction of the web. An
even flow of return air is achieved by arranging a
perforated plate into the suction chamber so that the
suction chamber is divided into
- an equalizing space surrounding the air distribution
channels in the space being formed between the perforated
plate and the web;
- a transport chamber being formed between the perforated
plate and the back side surface of the suction chamber.
For achieving a desired, even suction pressure profile, the
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open area of the perforated plate is dimensioned so that
return air is discharged evenly from the entire dryer area
through the perforated plate; whereby it is possible to
avoid flows and pressure variations in the vicinity of the
web, which are caused by uneven gathering of return air.
The open area of the perforated plate is typically under
15%, depending on the size of the suction chamber and the
air blow velocity of the nozzles. In a wedge-shaped suction
chamber, it is preferable to arrange a larger open area in
the perforated plate in the declining section of the
suction chamber than in the higher level section, so that
the open area may vary even extensively in the different
sections. When necessary, the perforated plate dividing the
suction chamber may be formed of several elements, modules,
arranged in succession in the transverse direction of the
web. The declining section of the suction chamber is then
provided with a perforated plate element, or module, which
has larger apertures or a larger number of apertures than
the perforated plate element arranged in the vicinity of
the suction box exit.
Now it has also been noticed that, in a two-stage dryer, in
which drying air is led directly from the side of the web
to a nozzle box extending over the web or to an air
distribution channel, the flow component of impingement air
discharging from the nozzles laterally to the web has a
considerable effect on the behavior of the web in the
flotation dryer. It has been found that straightening the
lateral flow component furthers the runnability of the
flotation dryer unit.
In a pref erred flotation dryer unit of the invention, the
nozzle element is thus provided with a so-called
straightening passage, with straightening elements for the
drying air flow fitted within, for eliminating or
substantially reducing such velocity component of the
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drying air flow fed towards the web through the nozzle,
that are directed laterally to the travel direction of the
web. With this arrangement, it is possible to prevent the
continuation of the effect of the axial velocity component
of drying air flowing in the nozzle boxes still in the air
flow discharging from the nozzle aperture, slot or holes.
With the arrangement of the invention, upon discharging air
from the nozzle aperture, drying or impingement air is
directed to flow so that its velocity component projected
to the web plane is parallel to the travel direction of the
web or that it forms an angle with the travel direction of
the web which is smaller than a marginal angle, e.g. of
t5°.
The straightening elements are typically formed of several
straightening channels arranged sequentially in the
transverse direction of the web, in which the flow is
typically arranged to travel principally perpendicularly to
the web plane or in a small angle to the web plane in a
plane which is parallel to the travel direction of the web
and principally perpendicular to the web plane. In vertical
direction, the straightening channels have to be
sufficiently long and narrow so that the desired
straightening effect will be achieved.
The straightening passage for the nozzle part is preferably
arranged in a slot limited by two wall elements parallel to
the nozzle box and extending across the web. The passage is
provided with several separate and sequential straightening
channels across the web by partitions extending from one
wall element to the other. The wall elements are
advantageously formed of an edge portion closest to the web
of the nozzle box side wall, or of a parallel plate-like
element attached to it. The wall elements are
advantageously arranged principally perpendicularly to the
web plane and the travel direction of the web but, if
desired, they may also be inclined.
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The partitions forming the straightening channels in the
straightening passage may typically be formed of a plate
profile parallel to the nozzle element, such as a so-called
fluted sheet, which is arranged into the slot between the
wall elements and bent to reciprocate in the slot and
across the slot from one wall element to another. One
fluted sheet may be long and folded several times to form
several sequential straightening channels. On the other
hand, the straightening channels may be formed of
sequential pieces of plate, each of them forming only one
or two partitions in the straightening passage.
The edge portions of the nozzle channel side walls, facing
the web, or the parallel plate-like elements joined to
them, typically have an extension extending from the plane
of the bottom portion towards the web, forming an angle of
< 90° with the planes of the bottom portions of the nozzle
elements, and forming the actual nozzle aperture. The
straightened gas flows coming from the straightening
channels discharge in the nozzle apertures in a way known
per se principally from a direction perpendicular to the
web to flows parallel to the web.
Also the return air flow may be adjusted by using flow
straighteners fitted between the nozzle boxes which may be
fluted sheets of the type described above.
The invention is above explained in an exemplary way by
referring to preferred embodiments of the invention, in
which the flotation dryer arrangement of the invention is
used for drying and heating a coated paper web by hot air.
The invention is naturally applicable in other similar
connections, for example, if the web is desired to be
treated with some other appropriate blowable gas than air.
The invention may also be used when cooling down the web
with blast air or some other gas.
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The flotation dryer unit of the invention may be single-
sided so that the flotation dryer unit or units are arran-
ged on one side of the web or, alternatively, double-sided
so that flotation dryer units are arranged opposite each
5 other on both sides of the web. If desired, it may also be
considered to use sequentially both flotation dryer units
and infra-dryer units for drying the paper web. On the
other hand, flotation dryer units may also be arranged in
a cylinder dryer to blow against the cylinder surface so
10 that nozzles are placed in an arched form corresponding to
the radius of the cylinder.
With the arrangement of the invention, it is possible to
considerably improve those properties of the flotation
dryer which are poorer in a conventional flotation dryer
than in an infra-dryer. With the invention, the size and
investment costs for the flotation dryer may thus be consi
derably reduced, and it is possible to increase its
specific vaporization efficiency and enhance its control
properties.
With the described two-stage structure, in which the air
distribution channels and nozzle parts of the flotation
dryer are integrated into each other as wedge-like nozzle
boxes extending across the web and which is provided with
a straightening of impingement air, an arrangement with a
substantially lower structure than the previously used
three-stage air-borne web-dryers is achieved. In a dryer
corresponding to the two-stage structure, the height of the
air flotation dryer box would be approximately 1.2 m on the
drive side and about 0.5 m on the tender side, the web path
width of the dryer being 8 m, the length of the flotation
dryer 2.4 m, and the blowing velocity 60 m/s; this is very
preferable when opening the boxes during a shutdown or a
break of the web. The flotation dryer unit of the invention
may thus be placed into smaller spaces than before.
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Because of the straightening elements fitted into the
nozzle elements of the nozzle boxes, air may, in the
arrangement of the invention, be distributed evenly by a
simple nozzle box structure, the investment costs of which
are low, even at high blowing velocities and temperatures,
i . a . with regard to large volumes of air . Also the fact ,
that the specific evaporation efficiency may be increased
by increasing the blowing velocities without the structure
of the flotation dryer becoming too big, may also be
considered to be an important advantage of the invention.
Due to its relatively small size, i.e. low structural mass,
the flotation dryer unit shown also reacts sensitively to
the adjustment of temperature. The flotation dryer warms up
quickly, for example, upon starting and after a break of
the web. A further advantage is that the flotation dryer
unit operates with a smaller pressure loss than the
previous three-stage arrangements so that blowing velocity
is achieved with less energy. This is due to the simple
two-stage structure which allows supply air to flow
relatively directly from the air distribution chamber to
the nozzle apertures.
Brief Description of the Drawings
The invention is next described in more detail, referring
to the enc7.osed drawings in which
Fig. 1 is an exemplary, schematic, partially cut-away
.:.perspective view of a ~ flotation dryer unit of the
.. invention;
,Fig. 2 is a schematic, vertical section of an air
flotation dryer box of the flotation dryer unit of
Fig. 1 in the transverse direction of the web;
Fig. 3 is a section of Fig. 2 in accordance with the line
p~o~;
Fig. 4 is an enlarged view of the detail shown with a
circle;
Fig. 5 is a section of Fig. 2 in accordance with the line
BB:
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Fig. 6 shows an enlarged part of a section of Fig. 2 in
accordance with the line CC;
Fig. 7 is a section of a second air flotation dryer box
of the invention in accordance with Fig. 6;
Fig. 8 is a section in accordance with Fig. 6 of a third
air flotation dryer box of the invention;
Fig. 9 is a section of Fig. 8 along the line DD;
Fig. 10 is a schematic perspective view of a part of a
straightening element available in the arrangement
of the invention;
Fig. 11 is a cross-section of Fig. 3 along the line EE;
and
Fig 12 is an enlarged view of a grate shown in Fig . 11
.
and seen~diagonally from the side.
Description
of
the
Preferred
Embodiments
Fig. 1 presents a flotation dryer unit 10 of the invention
for drying the coated web 12. The flotation dryer unit
comprises
several
nozzle
boxes
14
arranged
across
the
web,
through
Which
drying
air
jets
16
are
fed
towards
the
web.
The supply air distribution chamber 18 at the side of the
Web is common to all of the nozzle boxes 14 in the unit
.
The nozzle boxes 14 are covered with a box-like structure
opening
towards
the
web
and
forming
the
suction
chamber
20
for air being discharged from the web: The box-like
structure
of
the
auction
box
covers
the
nozzle
boxes
14,
:however,
leaving
a
free
space
for
the
discharge
of
return
air above the nozzle channels. Air is discharged from the
web area, as shown by big arrows, from the space 22 between
the nozzle boxes to the upper part of the suction chamber
and further to the gathering chamber 24 for return air on
the side of the web.
The nozzle boxes 14 are wedge-shaped, their height
decreasing from the entry end 26 towards the tail end 28,
i.e. in the flowing direction of supply air. In this case,
also the suction chamber 20 covering the nozzle boxes is
slightly wedge-shaped so that the height H of the suction
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chamber (Fig. 2) increases in the flowing direction of
return air. The entire air flotation dryer box is thus
wedge-shaped but, however, its height is considerably
smaller than a corresponding, conventional three-stage
flotation dryer structure.
In accordance with the invention, the suction box 20 is
divided into two parts by a perforated plate 30 equalizing
the flow of return air: to an equalizing space 32 between
the perforated plate 30 and the web 12, and to a transport
chamber 34 between the perforated plate and the back side
surface of the suction chamber 20. Both the equalizing
space 32 and the transport chamber 34 are, in the case
shown in Fig. 1, wedge-shaped so that their height
increases in the direction of the flow.
Fig. 2, in which the same reference numbers are used as in
Fig. 1, presents a cross-section of the flotation dryer
unit 10 of Fig. 1 taken in the transverse direction of the
web in the space 22 between the nozzle boxes. Fig. 2
describes in a better way than Fig. 1 how the perforated
plate 30, extending from one side of the web to the other,
divides the suction chamber 20 into an open equalizing
space 32 between the web and the perforated plate and into
the transport chamber 34 remaining between the perforated
plate and the back side surface of the suction chamber 20.
In the suction chamber, the perforated plate forms a
pressure equalizer thus providing an even flow of return
air in the entire web area.
The nozzle box 14 is shown in a side view in Fig. 2. It is
also seen that the perforated plate 30 is arranged into the
suction chamber within a small distance of, for example, 50
- 70 mm, above the nozzle boxes and principally parallel to
the upper surface of the nozzle boxes 14. The height h of
the nozzle boxes 14 and the height h' of the equalizing
space 32, which is slightly bigger than h, increase in the
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flow direction of return air principally in the same
proportion. The wedge-like shape of the cross-section of
the nozzle boxes 14 and the equalizing space 32 is thus
principally the same. Fig. 2 also shows that the air
transport chamber 34 is wedge-shaped, opening in the
direction of the return air flow.
It may also be seen in Fig. 2 that the nozzle channel 14 is
formed of an actual air distribution channel element 36 and
an actual nozzle element 38 below the air distribution
channel element.
Fig. 3 shows a section of the actual nozzles 38 of Fig. 2
in the direction of the web plane along the line AA. In
Fig. 3, there is shown a cross-section of six air
distribution channels 36 extending across the web. The air
distribution channels are connected to a common supply air
distribution chamber 18. Hot air, or some other appropriate
gas, is supplied to the flotation dryer through the air
distribution chamber, either directly from the source of
hot air, or as circulating air after conditioning of the
return air.
Fig. 4 shows the encircled area of Fig. 3, in which there
are two air distribution channels 36 and an intermediate
space 22. Also straightening passages 40 are marked in the
air distribution channels 36. The straightening passages
are provided with profile plates 42, e.g. fluted sheets
parallel to the passage. The profile plates are bent so
that the plate extends from one wall of the straightening
passage to the other, thus forming partitions 44 in the
passage. The partitions 44 divide the passages 40 into
separate straightening channel elements 46. The said
channel elements 46 divide the drying air flowing along the
air distribution channel 36 into successive, separate air
jets 16 flowing towards the web and shown in Fig. 1.
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Fig. 5 shows the cross-section of the suction chamber 20 of
Fig. 2 along the line BH. In the Figure, there is shown the
perforated plate 30 between the transport chamber of the
suction chamber and the equalizing space, with apertures
5 30'. Return air in accordance with the arrows flows from
the apertures 30' towards the gathering chamber 24 for
return air, from which return air is further led to the
discharge channel 48.
10 The size, number and reciprocal distance of the apertures
or openings in the perforated plate, may be calculated if
the amount of air discharging from the web and the width of
the web are known. The open area is typically less than 15
°s, which may be achieved, for example, with openings of 5 -
15 75 mm, preferably of 10 - 40 mm. However, the open area of
the perforated plate may vary in the transverse direction
of the web so that the open area decreases in the flowing
direction of return air.
Fig. 6 presents a cross-section of two boxes 14 parallel to
the travelling direction of the web. Each nozzle box has a
box-like structure, and is formed of two side walls 52, 54
extending across the web, of an upper part 56, which is
inclined in the longitudinal direction, and of a bottom
part 58. The inclination of the upper part 56 may be seen
in Figs 1 and 2. The nozzle box consists principally of two
parts, comprising an air distribution channel 36 and an
actual nozzle element 38 which is integrated into the air
distribution channel.
The nozzle element 38 is provided with straightening
passages or slots 40 extending across the web. The
straightening passages 40 are defined by planar wall
elements 60 across the web and joined to the web side lower
edges 52', 54' of the side walls 52 and 54 and parallel to
the said edge, and by second parallel planar wall elements
62 fitted into the nozzle element. The edges of the side
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walls 52 and 54 of the nozzle boxes may, if desired, be
directly used as wall elements defining the straightening
passage 40. The nozzles in Fig. 6 are overpressure nozzles
of the so-called Float type.
The straightening passages 40 are provided with elements 42
straightening the supply air flow; the said elements divide
the straightening passage into successive channel parts 46
by forming partitions 44, as is shown in Fig. 4.
The distance a between the wall elements 60 and 62 of the
straightening passage 40 is about 10 - 40 mm, preferably
- 25 mm. The height 1 of the straightening elements 42
arranged in the straightening passage 40, i.e. the depth of
15 the straightening channel, is about 30 - 100 mm, preferably
40 - 60 mm.
In addition, extensions 68 are provided to the planar
elements 60, the extensions together with the inner part 70
of the nozzle forming the actual nozzle apertures 72, from
which the straightened drying air is discharged towards the
web 12.
Fig. 6 further discloses a perforated plate 30 of the
invention provided with openings 30' and arranged above the
nozzle boxes 14. In accordance with the invention, the
perforated plate adjusts the return air flow via the spaces
22 between the nozzle boxes.
Fig. 7 presents a cross-section in accordance with Fig. 6
of two underpressure nozzles of the Foil type. In this
arrangement, the nozzle element 38 has only one
straightening passage 40, which is provided with an air
flow straightening element 42 for bringing air towards the
web 12 in a controllable way.
Extensions 52 " , 54 " of the part of the nozzle box side
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walls 54 and 52 facing the web are, in the application of
Fig. 7, bent to form a plane 64 parallel to the plane of
the supporting surface of the nozzle or to the web plane in
the space 22 between the adjacent nozzle boxes. The
extensions 52 " , 54 " form between them a return air gap 66
extending preferably across the web, from which return air
smoothly flows into the space 22 between the nozzle
channels. The return air gaps may be provided with a flow
straightening element.
Fig. 8 presents a cross-section in accordance with Fig. &
of two nozzle boxes 14 known in themselves, a perforated
plate 74 forming the actual nozzle apertures in the bottom
part of the boxes. A grate or a perforated plate 78 with a
large open area is arranged between the nozzle boxes to
prevent paper strips from flowing into the suction chamber.
The open area of the grate may be, for example, about 55 %,
which may be achieved with large openings 76 of, for
example, about 30 x 30 mm arranged with intervals of, for
example, 20 - 40 mm. The grate in Fig. 8 may also
advantageously be arranged, for example, between the nozzle
boxes shown in Fig. 6. The different intermediate space
arrangements for nozzle boxes shown in Figs 6, 7 and 8 are
also naturally suitable to be used in connection with also
other types of nozzles than those shown in the particular
ffigures.
Figs 9 and 10 show in more detail the structure of an
advantageous straightening element 42 of the invention.
Fig. 9 presents a cross-section along the line DD of the
straightening passage 40 in Fig. 8, which is provided with
straightening elements 42 with a curved entrance. The parts
44 extending across the passage 40 of the straightening
elements 42 form partitions in the passage, thus dividing
the passage into straightening channels 46.
In the case shown in Fig. 9, the partitions 44 are made
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arched in the incoming direction of the flow, parallel to
the flow, as is shown by the arrows indicating the flow.
The distance b between the partition walls is about 10 -
100 mm, typically about 20 - 50 mm. In this case, air flows
along the arch of the partitions without "disengaging" from
them and without creating turbulence in the straightening
channels 46 to a disturbing extent.
The partition arrangement in accordance with Fig. 9 is ac-
hieved with a straightening element 42 shown in Fig. 10.
The straightening element 42 consists of a plate which is
bent to alternately travel across the passage and along
either wall of the passage. The parts 80 travelling across
the passage are provided with extensions 82 directed
towards the incoming air flow, the extensions being
bendable so that they follow the direction of the air flaw.
In the arrangement shown in Fig. 9, the parts 84 travelling
along the walls are longer in the flow direction than the
parts 80 travelling across the passage, but, if so desired,
they may also be shorter.
The drying air flow coming from the air distribution
chamber is accelerated because of flow contraction caused
by openings 88 between the air distribution chamber 18 and
the air distribution channels 36. The said acceleration in
the supply air flow immediately after the inlet openings of
the nozzle boxes may, in some cases, cause an insufficient
velocity in the nozzle impingement profile in the first
part of the nozzle box. By dividing air from the supply air
distribution chamber 18 into distribution channels 36 in an
appropriate way, the said reduction in velocity may be
compensated.
Fig. 11 thus schematically shows a section along the line
EE taken from the wall between the supply air distribution
chamber 18 and the suction chamber 20 shown in Fig. 3. The
opening 88 is in an exemplary way provided with a grate 90
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for reducing the contraction of the entry flow into the air
distribution channel 36. In Fig. 12, the grate 90 is shown
enlarged and seen diagonally from the side. The width of
the grate is chosen taking into consideration the velocity
of the incoming flow, the width of the nozzles and the
length of the nozzles. The width of the grate apertures is
typically about 30 mm, and the length about 80 mm, but the
measures may vary according to need.
The lower plates 92 of the grate may be shaped to direct
the flow downwards so that they force part of the air flow
coming into the air distribution channel to flow towards
the actual nozzle 38 immediately after the opening. When
desired, longer guiding plates 94 may be joined to the
grate, forcing part of the air flows to turn towards the
nozzles. The guiding plates may be arranged to the height
of, for example, about 80 - 180 mm, preferably about 135
mm. The total length of the guiding plates and the grate
may be about 400 mm.
In the two-stage arrangements of the invention described
above, in which the nozzles 38 are integrated into parallel
air distribution channels 36 extending across the web, the
nozzles rnay be made easily detachable and changeable. The
nozzles may be supported at the inlet end for supply air,
i.e. at the drive side, and they may be arranged to be
suspended on the tender side. The replaceability of the
nozzles is especially important in drying processes in
which the nozzles easily get dirty and in which they have
to be cleaned in regular intervals.
The invention is above described referring to the enclosed
drawings. However, it is not in any way intended to limit
the invention to the exemplary arrangements and
embodiments. On the contrary, the purpose is to widely
apply the invention within the scope defined by the
enclosed claims.
